TW211020B - Dithiocarbamate polymers - Google Patents

Dithiocarbamate polymers Download PDF

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TW211020B
TW211020B TW081107533A TW81107533A TW211020B TW 211020 B TW211020 B TW 211020B TW 081107533 A TW081107533 A TW 081107533A TW 81107533 A TW81107533 A TW 81107533A TW 211020 B TW211020 B TW 211020B
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water
polymer
soluble
molecular weight
mole percent
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TW081107533A
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Chinese (zh)
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W Sparapany John
h collins John
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Nalco Chemical Co
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00Chemical modification by after-treatment
    • C08F8/34Introducing sulfur atoms or sulfur-containing groups
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/68Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
    • C02F1/683Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water by addition of complex-forming compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5272Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using specific organic precipitants
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/58Treatment of water, waste water, or sewage by removing specified dissolved compounds
    • C02F1/62Heavy metal compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G73/00Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
    • C08G73/02Polyamines
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S210/00Liquid purification or separation
    • Y10S210/902Materials removed
    • Y10S210/911Cumulative poison
    • Y10S210/912Heavy metal

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Medicinal Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Polymers & Plastics (AREA)
  • Inorganic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Removal Of Specific Substances (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

A water soluble ethylene dichloride ammonia polymer having a molecular weight of from 500 to 10,000 which contains from 5 to 50 mole % of dithiocarbamate salt groups. Also, disclosed are the use of these polymers in removing heavy metals from water.

Description

2110-,0 A6 B6 經濟部中央櫺準局Α工消費合作社印繁 五'發明説明() 本發明係有蘭廢水的處理。更特別者,本發明係有期 水溶性二磙代胺甲酸鹽聚合物及其在金羼淸除程序中的使 用方法。 隨著河流,水道等被工業廢水污染所引起的問題愈來 愈多,乃有愈靦厲的法規被制訂出來以避免這棰污染。如 今,將廢水中的金羼控制到低於其法定濃度之下已是一項 強制性要求。其中特別者,對於有害人類的重金屬,如汞 ,鎘,鋅,銅和鉻等已建立睹峻的法規。 已有多棰方法被提出來用Μ從廢水中脫除重金屬。於 一方法中,係用單純的二硫代胺甲酸鹽(如二甲基二碕代 胺甲酸鹽,DMDTC )來達到重金羼的脫除。使用低分子置 二硫代胺甲酸豔具有幾項缺點。其所形成的沈澱物可能係 小者,要將該沈澱物從廢水中沈著或遇濾出來可能會緩慢 。因此,要得到較快速的沈锻和過濾時,常需要另外添加 絮凝劑和/或促凝劑。 要增進二硫代胺甲酸鹽脫除金羼能力的一項提謙潙將 其與聚次乙基亞胺聚合物反應。這棰提議載於歐洲專利申 請0090551 Α1之中。此專利所述及的聚次乙基亞胺聚合物 係水不可溶者。雖然已證明具有蝥合不良性金颶的能力, 但螯合後的金屬/聚合物錯合物之分離卻相當地緩慢。這 類物質的作用據倍係類似於水不溶性離子交換樹脂的作用 〇 另一個聚次乙基亞胺-二硫代胺甲酸馥聚合物的例子 載於美國專利4,670, 160號中。於該專利的實施例8中, (請先閲讀背面之注意事項再璜寫本頁) 丨装· 訂· 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公贷) 3 81.9.25,000 A6 B6 經濟部中央樣準局R工消費合作社印製 2ΐί〇^^ 五、發明説明() 提及將分子量60,000的聚次乙基亞胺樹脂用二硫化硪予Μ 改質。完成後的樹脂雖證明具有某些水溶性,但仍含有實 質量的不溶性物質。 實驗數據指出雖然聚次乙基亞胺樹脂可用二硫化碩予 Μ改質而產生水溶性樹脂,但其分子量必須為約10,000或 以下。此外,可用的二硫化碩量為25克分子百分比或更低 〇 本發明的目的為提出聚合體型二硫代胺甲酸鹽聚合物 ,其為水溶性者且具有易於整合不良性重金屬使其易於從 水糸統中脫除之能力。 依此,本發明提出一種水溶性二氯乙烯/氨聚合物, 其特微在於具有分子量500到100,000且含有5到50克分子 百分比二硫代胺甲酸鹽基者。本發明也提出一種從含有重 金屬的水中脫除造些金靥的方法*其特徵在於包含下列步 教E : a) 用錯合用量的水溶性,分子量500到100,000且含 有5到50克分子百分比二硫代胺甲酸鹽基之二氣乙烯/氨 聚合物處理這類水以形成這些重金屬的錯合物;b)讓這 些錯合物從水中快速沈箸成爲沈澱物;及c).從水中分離 出該沈澱物。 二氯乙烯-氨聚合物 這種聚合物是經由二氯乙烯與氨的反應而製成者。後 文將閜述製成這類聚合物的典型反應。起始用的二氣乙烯 -氨聚合物通常具有500-100,000的分子量範圍。於一較 佳實施例中,其分子置為1,500到10,000,而其最適當的 (請先閲讀背面之注意事項再填寫本頁) i裝· 訂 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 4 81.9.25,000 21i ❶ Lv) A6 B6 五、發明説明() 分子量範圍則為1,500-5,000。爲了說明逭種聚合物的製 備,乃提出下面的實施例1。 審掄例1 於一壓力反應器中给入10.8重量炻含水氨,7.7重量 %無水氨,2.3重量%水和0.3重量% EDT A。将反應器密封 後加熱到115-1301:,再泵入二氯乙烯(EDC)。於添加入約 0.5重量%的£0(:之後,K約與EDC相同的速率加入50% 氫氧化納並在4.5小時内完成該項添加。該反應物添加期 間,採取其樣品。然後將這些樣品減壓濃縮以脫除殘餘的 EDC,NH3及反應副產物-氣乙烯。之後,用掖相餍析法和 聚乙二醇檷準品測量聚合物的重量平均分子量。製得一条 列聚合物,其組成與性質列於表1中。 (請t閲讀背面之注意事項再填窝本頁) 訂· 經濟部中央標準局貝工消費合作社印製 表1 搛S # wtXRnn Wt.XNanH \hL ttn. 聚合 分散麽 聚合物 同含最 1 12.9 10.4 1380 1010 1.3 41.2 2 15.4 12.3 1620 1100 1.5 46.4 3 17.5 15.2 1670 1100 1.5 41.9 4 20.2 19.3 1850 1290 1.6 43.1 5 22.3 23.1 2320 1290 1.8 37.8 6 24.7 25.7 2970 1440 2.0 47.1 7 26.7 27.4 3470 1540 2.2 41.5 8 29.2 29.2 4420 1700 2.6 42.5 9 32.1 32.8 6040 1910 3.1 37.9 10 33.8 34.6 7970 1910 4.2 36.5 11 36.3 42.6 92,100 2600 35.0 35.0 .气丨. 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 5 81.9.25,000 2ll〇r-° A6 B6 經濟部中央標準局貝工消费合作社印^ 五、發明説明() 用二硫化硪進行聚合物改質 聚胺類或聚亞胺類與二碕化硝反應Μ產生二硫代胺甲 酸酯或其鹽類係已熟知者。這棰反應,待別者,說明於美 國專利4,731, 187中;該專利因而列為本發明的參考資料 。聚胺與二碕化硪之間的反應較適當者係在溶劑,如水或 醇等之中進行。該反應在30-100t:溫度範圍内可順利進行 1到10小時之期間。在40-70Ό溫度下進行2到5小時可 逹到良好的轉化率。這些一般性反應條件可用Μ改質前文 所述及之二氣乙烯-氨聚合物。 製成的聚合物所含二硫代胺甲酸鹽基之克分子%通常 是在5到50克分子%範圍之内。其較適範圍為20-40克分 子%,而最適範圍為約25-35克分子%。 為了闌釋二氯乙烯聚合物轉化成二硫代胺甲酸鹽基之 反應,乃提出下面所述實施例2。 謇渝俐Ρ. 將38克50%氫氧化納和41克去離子水加到82克EDC/ ΝΗ3 聚合物上。將所得混合物置於壓力反應器中並加人14克二 硫化磺。然後,將該混合物加熱到45-50Ό三小時。在三 小時反應時間後,将該混合物冷卻並施Μ真空五分鐘以去 除殘餘二硫化碩。所得溶液型產物含有30%改質聚合物。 利用這種裂備技術,製備出下列改質聚合物:(參看 表2 ) ----------------^又 i (請也閲讀背面之注意事項再填寫本頁) i裝· 訂- 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公货) 6 81.9.25,000 Α6 Β6 五、發明説明( 表2 審掄俐 MJ. Mil K会物 an 50!KNanH 備詳 反産物f A 2970 22.1 8.0 21 21.7 可溶 B 2970 20.9 9.7 26 20.5 可溶 C 2970 18.0 11.1 35 22.3 可溶 D 3470 20.6 9.6 26 20.2 可溶 E 3420 18.9 11.7 35 18.5 可溶 F 4400 20.1 9.4 26 25.0 不可溶 G 4092 22.0 8.0 21 17.1 不可溶 Η 4096 22.0 8.0 10 17.1 可溶 I 1850 20.6 4.0 21 21.1 可溶 (請先閲讀背面之注意事項再填窝本頁) 經濟部中央橒準渴8工消費合作社印製 隨箸分子置的增加》可用來反應以形成水溶性反應產 物的二硫化碩用量即遞減。聚合物中的CSa含量低於约20 克分子下時《其金屬脫除效率會減低。 劑量 能從污染水中有效地脱除掉金羼的本發明改質聚合物 之用量通常係在每克分子欲處理的水所含重金屬用0.5到 3克分子聚合物之範圍内。一般而言,每克分子水中所含 重金羼用1到1·5克分子聚合物即可得到優良的結果。該 劑量可表成另一種形式,卽每克分子水中所含重金屬用3-10毫升0.3%聚合物活性溶液可μ產生令人谋意的金屬脫 除效果且使所形成的錯合物成為自我絮凝性者,亦即,可 快速沈著且易於從被處理水中分離出來。 本紙張尺度適用中固國家標準(CNS)甲4規格(210 X 297公釐) -1 - 81.9.25,0002110-, 0 A6 B6 Central Bureau of Economic Development, Ministry of Economic Affairs, Angong Consumer Cooperatives, Yinfan 5 'Description of the invention () This invention is the treatment of blue wastewater. More particularly, the present invention is a periodical water-soluble dioxocarbamate polymer and its method of use in a gold removal process. As rivers, waterways, etc. are more and more caused by industrial wastewater pollution, more and more vigorous regulations have been formulated to avoid this pollution. Today, it is a mandatory requirement to control the Jinyong in wastewater below its legal concentration. Among them, special regulations have been established for heavy metals harmful to humans, such as mercury, cadmium, zinc, copper and chromium. Multiple methods have been proposed to use M to remove heavy metals from wastewater. In one method, a simple dithiocarbamate (such as dimethyldiaminocarbamate, DMDTC) is used to achieve heavy gold removal. The use of low molecular weight dithiocarbamic acid has several disadvantages. The precipitate formed may be a small one, and it may be slow to settle the sediment from the waste water or filter it out. Therefore, in order to obtain faster sinking and filtering, it is often necessary to add additional flocculants and / or accelerators. To improve the ability of dithioamine formate to remove gold ions, it is reacted with polyethylenimine polymer. This proposal is contained in European Patent Application 0009551 A1. The polyethylenimine polymer described in this patent is water-insoluble. Although it has been shown to have the ability to inhibit mal-competitive gold hurricanes, the separation of chelated metal / polymer complexes is quite slow. The function of this type of material is similar to that of water-insoluble ion exchange resins. Another example of polyethylenimine-dithiocarbamate polymer is contained in U.S. Patent No. 4,670,160. In Example 8 of the patent, (please read the precautions on the back before writing this page) 丨 Install · Order · This paper size is applicable to China National Standard (CNS) Grade 4 (210 X 297 public loan) 3 81.9 .25,000 A6 B6 Printed by the R & C Consumer Cooperative of the Central Prototype Bureau of the Ministry of Economic Affairs. 5. Description of the invention () It is mentioned that the polyethylenimine resin with a molecular weight of 60,000 is modified with M disulfide. Although the completed resin proved to be somewhat water-soluble, it still contained substantial amounts of insoluble materials. The experimental data indicates that although the polyethylenimine resin can be modified with M2S to produce a water-soluble resin, its molecular weight must be about 10,000 or less. In addition, the available amount of disulfide is 25 mol% or less. The purpose of the present invention is to propose a polymer-type dithiocarbamate polymer which is water-soluble and has poor integration of heavy metals making it easy Ability to be removed from the water system. According to this, the present invention proposes a water-soluble dichloroethylene / ammonia polymer, which is characterized in that it has a molecular weight of 500 to 100,000 and contains 5 to 50 mole percent of dithiocarbamate groups. The present invention also proposes a method for removing some gold tallow from water containing heavy metals * which is characterized by the following steps E: a) Water solubility with a mismatch amount, a molecular weight of 500 to 100,000 and containing 5 to 50 mole percent Dithiocarbamate-based two-gas ethylene / ammonia polymer treats this type of water to form complexes of these heavy metals; b) allows these complexes to quickly settle into precipitates from water; and c). The precipitate was separated in water. Vinyl chloride-ammonia polymer This polymer is made by the reaction of vinyl chloride and ammonia. The typical reactions of such polymers will be described later. The starting two-gas ethylene-ammonia polymer usually has a molecular weight range of 500-100,000. In a preferred embodiment, the numerator is set to 1,500 to 10,000, and its most appropriate (please read the precautions on the back and then fill out this page) i Packed · The size of the paper is applicable to China National Standard (CNS) A 4 Specifications (210 X 297 mm) 4 81.9.25,000 21i ❶ Lv) A6 B6 5. Description of the invention () The molecular weight range is 1,500-5,000. In order to illustrate the preparation of the seed polymer, the following Example 1 is proposed. Trial Example 1 In a pressure reactor, 10.8% of the weight of water-containing ammonia, 7.7% by weight of anhydrous ammonia, 2.3% by weight of water and 0.3% by weight of EDT A were fed. Seal the reactor and heat to 115-1301 :, then pump in ethylene dichloride (EDC). After adding about 0.5% by weight of £ 0 (: After that, add 50% sodium hydroxide at the same rate as EDC and complete the addition within 4.5 hours. During the addition of the reactants, take samples of them. Then these The sample was concentrated under reduced pressure to remove residual EDC, NH3 and reaction by-product-gaseous ethylene. After that, the weight average molecular weight of the polymer was measured by the phase analysis and polyethylene glycol standard. A series of polymers was prepared , Its composition and properties are listed in Table 1. (Please read the precautions on the back and fill in this page) Order · Printed by the Ministry of Economic Affairs Central Standards Bureau Beigong Consumer Cooperatives 1 搛 S # wtXRnn Wt.XNanH \ hL ttn .Polymerization and dispersion of the same polymer 1 12.9 10.4 1380 1010 1.3 41.2 2 15.4 12.3 1620 1100 1.5 46.4 3 17.5 15.2 1670 1100 1.5 41.9 4 20.2 19.3 1850 1290 1.6 43.1 5 22.3 23.1 2320 1290 1.8 37.8 6 24.7 25.7 2970 1440 2.0 47.1 7 26.7 27.4 3470 1540 2.2 41.5 8 29.2 29.2 4420 1700 2.6 42.5 9 32.1 32.8 6040 1910 3.1 37.9 10 33.8 34.6 7970 1910 4.2 36.5 11 36.3 42.6 92,100 2600 35.0 35.0 National Standards (CNS) A4 specifications (210 X 297 mm) 5 81.9.25,000 2ll〇r- ° A6 B6 Printed by the Beigong Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs ^ V. Description of invention () Polymerization with disulfide The reaction of modified polyamines or polyimines with dinitrated nitric acid to produce dithiocarbamate or its salts is well known. This reaction, described elsewhere, is described in US Patent 4,731,187 The patent is therefore listed as a reference for the present invention. The reaction between polyamine and diamine is more appropriate in a solvent such as water or alcohol. The reaction is within the range of 30-100t: temperature It can be carried out smoothly for a period of 1 to 10 hours. Good conversion can be achieved at a temperature of 40-70 ° C for 2 to 5 hours. These general reaction conditions can be modified with M2 to improve the second gas ethylene-ammonia polymer mentioned above. The mol% of the dithiocarbamate group contained in the finished polymer is usually in the range of 5 to 50 mol%. The more suitable range is 20-40 mol%, and the most suitable range is about 25 -35 mol%. For conversion of vinyl chloride polymer to dithiocarbamate group The reaction is to propose Example 2 described below. Jian Yuli P. Add 38 grams of 50% sodium hydroxide and 41 grams of deionized water to 82 grams of EDC / NH3 polymer. The resulting mixture was placed in a pressure reactor and 14 grams of sulfur disulfide was added. Then, the mixture was heated to 45-50 ° C for three hours. After a reaction time of three hours, the mixture was cooled and vacuum was applied for five minutes to remove residual disulfide. The resulting solution product contains 30% modified polymer. Using this split preparation technology, the following modified polymers were prepared: (see Table 2) ---------------- ^ Youi (please also read the notes on the back and fill in this Page) i Pack · Order-This paper scale is applicable to the Chinese National Standard (CNS) A 4 specifications (210 X 297 public goods) 6 81.9.25,000 Α6 Β6 V. Description of the invention (Table 2 Examined by MJ. Mil K 会 物 an 50! KNanH Detailed counterproduct f A 2970 22.1 8.0 21 21.7 soluble B 2970 20.9 9.7 26 20.5 soluble C 2970 18.0 11.1 35 22.3 soluble D 3470 20.6 9.6 26 20.2 soluble E 3420 18.9 11.7 35 18.5 soluble F 4400 20.1 9.4 26 25.0 Insoluble G 4092 22.0 8.0 21 17.1 Insoluble H 4096 22.0 8.0 10 17.1 Soluble I 1850 20.6 4.0 21 21.1 Soluble (please read the precautions on the back before filling this page) Central Ministry of Economic Affairs 8 Printing and Printing by the Consumer Cooperative Co., Ltd. with the increase of the molecular weight of the cistern "can be used to react to form a water-soluble reaction product. The amount of disulfide is decreasing. When the CSa content in the polymer is less than about 20 mol, the metal removal efficiency It will be reduced. The dose can effectively remove Jin Yun's hair from contaminated water The amount of modified polymer is usually in the range of 0.5 to 3 gram of polymer per gram of heavy metal contained in the water to be treated. Generally speaking, 1 to 1.5 grams of heavy gold per mol of water Excellent results can be obtained with molecular polymers. The dosage can be expressed in another form. 3-10 ml of 0.3% polymer active solution per gram of molecular water can produce a surprising metal removal effect. And make the formed complex into self-flocculation, that is, it can be quickly settled and easily separated from the treated water. This paper scale is applicable to China Solid National Standard (CNS) A 4 specifications (210 X 297 mm) -1-81.9.25,000

五、發明說明() 寘施例3 為了說明表2所列胺甲酸鹽聚合物有效地從供给水中 轚合並脫除網金羼之能力,将其相期數據呈列於表3中。 表3 铪人污染水纒餘铟(oDn) 聚会物瀧鼉fag) / 100·丨睡水 聚合物 0 6 9 12 15 18 A 20 — 1.1 0.09 0.05 一 B 20 3.9 0.2 0.07 0.07 0.05 C 20 3.1 0.2 0.06 0.05 0.05 D 20 3.4 0.1 0.06 0.04 0.04 E 20 2.2 0.11 4.06 0.06 0.06 Η 20 一 0.14 0.08 0.08 — <請先聞$面之注$项再本I) -丨裝- 訂· «濟部中央螵準房R工消費合作杜印製 必須特別提及者為所觀察到的過濾速率係快速者。 本發明的優點 1. EDC/HH3聚合物可用csa在溫和條件下衍化而形成水 溶性聚合涯型二硫代胺甲酸鹽聚合物。 2. 該聚合體型二硫代胺甲酸锂可以比DMDTC (小分子) 更快速地將重金屬從廢水中螯合且沈澱出來,這點從沈澱 物的快速形成即可明證。 3. 聚合龉型二硫代胺甲酸鹽除了具有良好的螯合能力之 外,所形成的沈澱物也比DMDTC所産生者較為大且沈著得 非常快速。因為沈澱物大,所以不需要加入促凝劑或絮凝 一 8 一 線· 衣纸張/L度適用中國圔家標準(CNS>甲4规格(210 X 297公* ) 82.3. 40.000 公\1〇一ο 五、發明説明() 劑來幫助沈著。因此之故,本發明聚合體型二硫代胺甲酸 鹽可為用Μ從廢水中脫除重金羼之箪一產品,單一步驟處 理型化學品。 (請先聞讀背面之注意事項再璜寫本Τ) —装· 訂· 蛭濟部中央標準局员工消費合作社印製 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐) 9 81.9.25,000V. Description of the invention () Example 3 In order to illustrate the ability of the urethane polymers listed in Table 2 to effectively remove and retreat from the supply water, the phase data is presented in Table 3. Table 3 Hafnium polluted water, indium (oDn), party material, taki (fag) / 100 · 丨 Sleep water polymer 0 6 9 12 15 18 A 20 — 1.1 0.09 0.05 1 B 20 3.9 0.2 0.07 0.07 0.05 C 20 3.1 0.2 0.06 0.05 0.05 D 20 3.4 0.1 0.06 0.04 0.04 E 20 2.2 0.11 4.06 0.06 0.06 Η 20 one 0.14 0.08 0.08 — < please first hear the $ 面 之 注 $ item and then I)-丨 Installation- Order The quasi-room R-consumer cooperation du printing must mention in particular that the observed filtration rate is fast. Advantages of the invention 1. The EDC / HH3 polymer can be derivatized under csa under mild conditions to form a water-soluble polymerized dithioamine formate polymer. 2. The polymer-type lithium dithiocarbamate can chelate and precipitate heavy metals from wastewater faster than DMDTC (small molecules), as evidenced by the rapid formation of precipitates. 3. In addition to its good chelating ability, the polymerized dithiocarbamate also has a larger precipitate than the one produced by DMDTC and settles very quickly. Because of the large sediments, there is no need to add accelerators or flocculation. The first line · clothing paper / L degree is applicable to the Chinese standard (CNS> A 4 specifications (210 X 297 g *)) 82.3. 40.000 g \ 1〇 一ο Fifth, the description of the invention () agent to help deposition. Therefore, the polymer-type dithiocarbamate of the present invention can be a single-step treatment type chemical that uses M to remove heavy gold from the wastewater. (Please read the precautions on the back before writing this book)-Binding · Order · Printed by the Staff Consumption Cooperative of the Central Standards Bureau of the Ministry of Economy and Economy. The size of the paper is in accordance with China National Standard (CNS) Grade 4 (210 X 297 mm) 9 81.9.25,000

Claims (1)

六、申請專利範園 1. 一種水溶性二氯乙烯-氨聚合物,其特戡在於具有 500到100, 〇〇〇之分子量及含有5到50克分子百分比的 二碕代胺甲酸鹽基。 2. 如申請專利範圍第i項的水溶性二氯乙烯-氨聚合物 ,其特戡在於其分子量為1500到10,000且其含有15到 50克分子百分比的二碕代胺甲酸鹽基。 3. 如申請專利範圍第1項的水溶性二氯乙烯-氨聚合物 ,其特擞在於其分子量為1500到5000且其含有約25到 40克分子百分比的二硫代胺甲酸麴基。 4. 一種從含有重金属的水中脫除這些金羼的方法,其特 勸在於包含下列步驟:a) 用錯合作用量,具有500 到100,000且含有5到50克分子百分比二硫代胺甲酸 鹽基的水溶性二氣乙烯-氨聚合物處理該水Μ形成這 些重金屬的錯合物;b)讓這種錯合物從水中快速沈 著成為沈澱物;及c)將該沈澱物從水中分離出來。 5. 如申請專利範圍第4項的方法,其特擞在於該水溶性 聚合物具有1500到10,000的分子量且其含有15到50克 分子百分比的二硫代胺甲酸鹽基。 6. 如申請專利範圍第4項的方法《其中該水溶性聚合物 具有1500到5000的分子量且含有約25到40克分子百分 比的二碕代胺甲酸鹽基。 (請先閱讀背面之注意事項再填寫本頁) •訂· .線· 經濟部中央搮準局印製 f 4 (210X297 公廣) 10 78. 8. 3,0006. Patent application Fan Yuan 1. A water-soluble dichloroethylene-ammonia polymer, which is characterized in that it has a molecular weight of 500 to 100, 000 and contains 5 to 50 mole percent of diamine amine formate group . 2. The water-soluble dichloroethylene-ammonia polymer of item i in the scope of patent application is characterized in that its molecular weight is 1500 to 10,000 and it contains 15 to 50 mole percent of diaminoamine formate groups. 3. The water-soluble dichloroethylene-ammonia polymer as claimed in item 1 of the patent application is characterized in that its molecular weight is 1500 to 5000 and it contains approximately 25 to 40 mole percent of dithiocarbamate. 4. A method for removing these gold ions from heavy metal-containing water, the particular advice is to include the following steps: a) Use a mismatched amount of 500 to 100,000 and contain 5 to 50 mole percent of dithiocarbamate The water-soluble difluoroethylene-ammonia polymer treats the water M to form complexes of these heavy metals; b) allows the complex to rapidly precipitate from the water into a precipitate; and c) separates the precipitate from the water . 5. The method as claimed in item 4 of the patent application is characterized in that the water-soluble polymer has a molecular weight of 1500 to 10,000 and it contains 15 to 50 mole percent of dithiocarbamate groups. 6. As in the method of claim 4 of the patent application, wherein the water-soluble polymer has a molecular weight of 1500 to 5000 and contains about 25 to 40 mole percent of dibenzylamine formate groups. (Please read the precautions on the back before filling in this page) • Order · Line · Printed by the Central Bureau of Economic Affairs of the Ministry of Economic Affairs f 4 (210X297 Public Broadcasting) 10 78. 8. 3,000
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